Tetrafluoropropene compositions and uses thereof

ABSTRACT

The present invention relates to compositions for use in refrigeration, air-conditioning, and heat pump systems wherein the composition comprises a tetrafluoropropene and at least one other component. The compositions of the present invention are useful in processes for producing cooling or heat, as heat transfer fluids, foam blowing agents, aerosol propellants, and fire suppression and fire extinguishing agents.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No. 14/499,454, filed Sep. 29, 2014, now U.S. Pat. No. 9,540,556, which is a divisional of U.S. patent application Ser. No. 13/858,182, filed Apr. 8, 2013, abandoned, which is a divisional of U.S. patent application Ser. No. 12/618,890, filed Nov. 16, 2009, abandoned, which claims the priority benefit of U.S. Provisional Patent Application No. 61/116,029, filed Nov. 19, 2008, and U.S. Provisional Patent Application No. 61/180,281, filed May 21, 2009.

BACKGROUND

1. Field of the Disclosure

The present disclosure relates to compositions for use in refrigeration, air-conditioning, and heat pump systems wherein the composition comprises a tetrafluoropropene and at least one other compound. The compositions of the present invention are useful in processes for producing cooling or heat, as heat transfer fluids, foam blowing agents, aerosol propellants, and fire suppression and fire extinguishing agents.

2. Description of Related Art

The refrigeration industry has been working for the past few decades to find replacement refrigerants for the ozone depleting chlorofluorocarbons (CFCs) and hydrochlorofluorocarbons (HCFCs) being phased out as a result of the Montreal Protocol. The solution for most refrigerant producers has been the commercialization of hydrofluorocarbon (HFC) refrigerants. The new HFC refrigerants, HFC-134a being the most widely used at this time, have zero ozone depletion potential and thus are not affected by the current regulatory phase out as a result of the Montreal Protocol.

Further environmental regulations may ultimately cause global phase out of certain HFC refrigerants. Currently, the automobile industry is facing regulations relating to global warming potential for refrigerants used in mobile air-conditioning. Therefore, there is a great current need to identify new refrigerants with reduced global warming potential for the mobile air-conditioning market. Should the regulations be more broadly applied in the future, for instance for stationary air conditioning and refrigeration systems, an even greater need will be felt for refrigerants that can be used in all areas of the refrigeration and air-conditioning industry.

Currently proposed replacement refrigerants for HFC-134a include HFC-152a, pure hydrocarbons such as butane or propane, or “natural” refrigerants such as CO₂. Many of these suggested replacements are toxic, flammable, and/or have low energy efficiency. New replacements are also being proposed for HCFC-22, R404A, R407C, and R410A among others. Therefore, new alternative refrigerants are being sought.

BRIEF SUMMARY

The object of the present disclosure is to provide novel refrigerant compositions and heat transfer fluid compositions that provide unique characteristics to meet the demands of low or zero ozone depletion potential and lower global warming potential as compared to current refrigerants.

Disclosed are compositions selected from the group consisting of compositions comprising:

-   -   HFO-1234yf, HFC-152a, and HFC-134a;     -   HFO-1234yf, HFC-125, and HFC-152a;     -   HFO-1234yf, HFC-125, and HFC-134a;     -   HFO-1234yf, HFC-32, and HFC-134a;     -   HFO-1234yf, HFC-32, HFC-125, and HFC-134a;     -   HFO-1234ze and HFC-32;     -   HFO-1234ze and HFC-125;     -   HFO-1234ze, HFC-125, and HFC-152a;     -   HFO-1234ze, HFC-125, and HFC-134a;     -   HFO-1234ze, HFC-32, and HFC-134a;     -   and     -   HFO-1234ze, HFC-32, HFC-125, and HFC-134a.

Also disclosed are non-flammable compositions comprising no more than about 60 weight percent HFO-1234yf and at least about 40 weight percent HFC-134a.

Also disclosed are compositions comprising at least about 85 weight percent HFO-1234yf and up to about 15 weight percent HFC-32.

DETAILED DESCRIPTION

Before addressing details of embodiments described below, some terms are defined or clarified.

Definitions

As used herein, the term heat transfer composition means a composition used to carry heat from a heat source to a heat sink.

A heat source is defined as any space, location, object or body from which it is desirable to add, transfer, move or remove heat. Examples of heat sources is spaces (open or enclosed) requiring refrigeration or cooling, such as refrigerator or freezer cases in a supermarket, building spaces requiring air-conditioning, industrial water chillers or the passenger compartment of an automobile requiring air-conditioning. In some embodiments, the heat transfer composition may remain in a constant state throughout the transfer process (i.e., not evaporate or condense). In other embodiments, evaporative cooling processes may utilize heat transfer compositions as well.

A heat sink is defined as any space, location, object or body capable of absorbing heat. A vapor compression refrigeration system is one example of such a heat sink.

A heat transfer system is the system (or apparatus) used to produce a heating or cooling effect in a particular space. A heat transfer system may be a mobile system or a stationary system.

Examples of heat transfer systems included but are not limited to air conditioners, freezers, refrigerators, heat pumps, water chillers, flooded evaporator chillers, direct expansion chillers, walk-in coolers, mobile refrigerators, mobile air conditioning units, dehumidifiers, and combinations thereof.

As used herein, mobile heat transfer system refers to any refrigeration, air conditioner, or heating apparatus incorporated into a transportation unit for the road, rail, sea or air. In addition, mobile refrigeration or air conditioner units, include those apparatus that are independent of any moving carrier and are known as “intermodal” systems. Such intermodal systems include “container’ (combined sea/land transport) as well as “swap bodies” (combined road/rail transport).

As used herein, stationary heat transfer systems are systems that are fixed in place during operation. A stationary heat transfer system may be associated within or attached to buildings of any variety or may be stand alone devices located out of doors, such as a soft drink vending machine. These stationary applications may be stationary air conditioning and heat pumps (including but not limited to chillers, high temperature heat pumps, residential, commercial or industrial air conditioning systems, and including window, ductless, ducted, packaged terminal, chillers, and those exterior but connected to the building such as rooftop systems). In stationary refrigeration applications, the disclosed compositions may be useful in equipment including commercial, industrial or residential refrigerators and freezers, ice machines, self-contained coolers and freezers, flooded evaporator chillers, direct expansion chillers, walk-in and reach-in coolers and freezers, and combination systems. In some embodiments, the disclosed compositions may be used in supermarket refrigeration systems. Additionally, stationary applications may utilize a secondary loop system that uses a primary refrigerant to produce cooling in one location that is transferred to a remote location via a secondary heat transfer fluid.

Refrigeration capacity (sometimes referred to as cooling capacity) is a term to define the change in enthalpy of a refrigerant in an evaporator per pound of refrigerant circulated, i.e., the heat removed by the refrigerant in the evaporator per a given time. The refrigeration capacity is a measure of the ability of a refrigerant or heat transfer composition to produce cooling. Therefore, the higher the capacity the greater the cooling that is produced.

Coefficient of performance (COP) is the amount of heat removed divided by the required energy input to operate the cycle. The higher the COP, the higher is the energy efficiency. COP is directly related to the energy efficiency ratio (EER) that is the efficiency rating for refrigeration or air conditioning equipment at a specific set of internal and external temperatures.

The term “subcooling” is meant the reduction of the temperature of a liquid below that liquid's saturation point for a given pressure. The saturation point is the temperature at which the vapor is completely condensed to a liquid, but subcooling (continues to cool the liquid to a lower temperature liquid at the given pressure. By cooling a liquid below the saturation temperature (or bubble point temperature), the net refrigeration capacity can be increased. Subcooling thereby improves refrigeration capacity and energy efficiency of a system. Subcool amount is the amount of cooling below the saturation temperature (in degrees).

Superheat is a term that defines how far above its saturation vapor temperature (the temperature at which, if the composition is cooled, the first drop of liquid is formed, also referred to as the “dew point”) a vapor composition is heated.

Temperature glide (sometimes referred to simply as “glide”) is the absolute value of the difference between the starting and ending temperatures of a phase-change process by a refrigerant within a component of a refrigerant system, exclusive of any subcooling or superheating. This term may be used to describe condensation or evaporation of a near azeotropic or non-azeotropic composition.

By azeotropic composition is meant a constant-boiling mixture of two or more substances that behave as a single substance. One way to characterize an azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has the same composition as the liquid from which it is evaporated or distilled, i.e., the mixture distills/refluxes without compositional change. Constant-boiling compositions are characterized as azeotropic because they exhibit either a maximum or minimum boiling point, as compared with that of the non-azeotropic mixture of the same compounds. An azeotropic composition will not fractionate within a refrigeration or air conditioning system during operation. Additionally, an azeotropic composition will not fractionate upon leakage from a refrigeration or air conditioning system.

A near-azeotropic composition (also commonly referred to as an “azeotrope-like composition”) is a substantially constant boiling liquid admixture of two or more substances that behaves essentially as a single substance. One way to characterize a near-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has substantially the same composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes without substantial composition change. Another way to characterize a near-azeotropic composition is that the bubble point vapor pressure and the dew point vapor pressure of the composition at a particular temperature are substantially the same. Herein, a composition is near-azeotropic if, after 50 weight percent of the composition is removed, such as by evaporation or boiling off, the difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed is less than about 10 percent.

A non-azeotropic composition is a mixture of two or more substances that behaves as a simple mixture rather than a single substance. One way to characterize a non-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has a substantially different composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes with substantial composition change. Another way to characterize a non-azeotropic composition is that the bubble point vapor pressure and the dew point vapor pressure of the composition at a particular temperature are substantially different. Herein, a composition is non-azeotropic if, after 50 weight percent of the composition is removed, such as by evaporation or boiling off, the difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed is greater than about 10 percent.

As used herein, the term “lubricant” means any material added to a composition or a compressor (and in contact with any heat transfer composition in use within any heat transfer system) that provides lubrication to the compressor to aid in preventing parts from seizing.

As used herein, compatibilizers are compounds which improve solubility of the hydrofluorocarbon of the disclosed compositions in heat transfer system lubricants. In some embodiments, the compatibilizers improve oil return to the compressor. In some embodiments, the composition is used with a system lubricant to reduce oil-rich phase viscosity.

As used herein, oil-return refers to the ability of a heat transfer composition to carry lubricant through a heat transfer system and return it to the compressor. That is, in use, it is not uncommon for some portion of the compressor lubricant to be carried away by the heat transfer composition from the compressor into the other portions of the system. In such systems, if the lubricant is not efficiently returned to the compressor, the compressor will eventually fail due to lack of lubrication.

As used herein, “ultra-violet” dye is defined as a UV fluorescent or phosphorescent composition that absorbs light in the ultra-violet or “near” ultra-violet region of the electromagnetic spectrum. The fluorescence produced by the UV fluorescent dye under illumination by a UV light that emits at least some radiation with a wavelength in the range of from 10 nanometers to about 775 nanometers may be detected.

Flammability is a term used to mean the ability of a composition to ignite and/or propagate a flame. For refrigerants and other heat transfer compositions, the lower flammability limit (“LFL”) is the minimum concentration of the heat transfer composition in air that is capable of propagating a flame through a homogeneous mixture of the composition and air under test conditions specified in ASTM (American Society of Testing and Materials) E681. The upper flammability limit (“UFL”) is the maximum concentration of the heat transfer composition in air that is capable of propagating a flame through a homogeneous mixture of the composition and air under the same test conditions. The flammability test, ASTM E681, is run on the liquid phase and the vapor phase present in a closed container above the liquid at specified temperatures as designated by ASHRAE (American Society of Heating, Refrigerating and Air-Conditioning Engineers) in the ASHRAE Standard 34. In order to be classified by ASHRAE as non-flammable, a refrigerant must be non-flammable under the conditions of ASTM E681 as formulated in both the liquid and vapor phase as well as during leakage scenarios.

Global warming potential (GWP) is an index for estimating relative global warming contribution due to atmospheric emission of a kilogram of a particular greenhouse gas compared to emission of a kilogram of carbon dioxide. GWP can be calculated for different time horizons showing the effect of atmospheric lifetime for a given gas. The GWP for the 100 year time horizon is commonly the value referenced. For mixtures, a weighted average can be calculated based on the individual GWPs for each component.

Ozone depletion potential (ODP) is a number that refers to the amount of ozone depletion caused by a substance. The ODP is the ratio of the impact on ozone of a chemical compared to the impact of a similar mass of CFC-11 (fluorotrichloromethane). Thus, the ODP of CFC-11 is defined to be 1.0. Other CFCs and HCFCs have ODPs that range from 0.01 to 1.0. HFCs have zero ODP because they do not contain chlorine.

As used herein, the terms “comprises,” “comprising,” “includes,” “including,” “has,” “having” or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a composition, process, method, article, or apparatus that comprises a list of elements is not necessarily limited to only those elements but may include other elements not expressly listed or inherent to such composition, process, method, article, or apparatus. Further, unless expressly stated to the contrary, “or” refers to an inclusive or and not to an exclusive or. For example, a condition A or B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present), and both A and B are true (or present).

The transitional phrase “consisting of” excludes any element, step, or ingredient not specified. If in the claim such would close the claim to the inclusion of materials other than those recited except for impurities ordinarily associated therewith. When the phrase “consists of” appears in a clause of the body of a claim, rather than immediately following the preamble, it limits only the element set forth in that clause; other elements are not excluded from the claim as a whole.

The transitional phrase “consisting essentially of” is used to define a composition, method or apparatus that includes materials, steps, features, components, or elements, in addition to those literally disclosed provided that these additional included materials, steps, features, components, or elements do materially affect the basic and novel characteristic(s) of the claimed invention. The term ‘consisting essentially of’ occupies a middle ground between “comprising” and ‘consisting of’.

Where applicants have defined an invention or a portion thereof with an open-ended term such as “comprising,” it should be readily understood that (unless otherwise stated) the description should be interpreted to also describe such an invention using the terms “consisting essentially of” or “consisting of.”

Also, use of “a” or “an” are employed to describe elements and components described herein. This is done merely for convenience and to give a general sense of the scope of the invention. This description should be read to include one or at least one and the singular also includes the plural unless it is obvious that it is meant otherwise.

Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Although methods and materials similar or equivalent to those described herein can be used in the practice or testing of embodiments of the disclosed compositions, suitable methods and materials are described below. All publications, patent applications, patents, and other references mentioned herein are incorporated by reference in their entirety, unless a particular passage is cited. In case of conflict, the present specification, including definitions, will control. In addition, the materials, methods, and examples are illustrative only and not intended to be limiting.

Compositions

Disclosed are compositions comprising tetrafluoropropene and at least one other compound. Tetrafluoropropene may be either 1,3,3,3-tetrafluoropropene (HFO-1234ze) or 2,3,3,3-tetrafluoropropene (HFO-1234yf). HFO-1234ze may exist as different configurational isomers, E- (trans-) or Z- (cis-), or stereoisomers. The present invention is intended to include all single configurational isomers, single stereoisomers or any combination or mixture thereof.

Both HFO-1234ze and HFO-1234yf may be made by methods known in the art.

The disclosed compositions also contain other fluorinated compounds selected from the group consisting of difluoromethane (HFC-32), tetrafluoroethane, pentafluoroethane (HFC-125), and difluoroethane (1,1-difluoroethane or HFC-152a). Tetrafluoroethane may be 1,1,1,2-tetrafluoroethane (HFC-134a) or 1,1,2,2-tetrafluoroethane (HFC-134). These fluorinated compounds are commercially available or may be made by methods known in the art.

In one embodiment, compositions are disclosed comprising:

HFO-1234yf and HFC-32;

HFO-1234yf and HFC-134a;

HFO-1234yf, HFC-152a, and HFC-134a;

HFO-1234yf, HFC-125, and HFC-152a;

HFO-1234yf, HFC-125, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-125;

HFO-1234yf, HFC-32, HFC-125, and HFC-134a;

HFO-1234ze and HFC-32;

HFO-1234ze and HFC-125;

HFO-1234ze, HFC-125, and HFC-152a;

HFO-1234ze, HFC-125, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-125; and

HFO-1234ze, HFC-32, HFC-125, and HFC-134a.

In another embodiment, compositions are disclosed consisting essentially of:

HFO-1234yf and HFC-32;

HFO-1234yf and HFC-134a;

HFO-1234yf, HFC-152a, and HFC-134a;

HFO-1234yf, HFC-125, and HFC-152a;

HFO-1234yf, HFC-125, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-125;

HFO-1234yf, HFC-32, HFC-125, and HFC-134a;

HFO-1234ze and HFC-32;

HFO-1234ze and HFC-125;

HFO-1234ze, HFC-125, and HFC-152a;

HFO-1234ze, HFC-125, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-125; and

HFO-1234ze, HFC-32, HFC-125, and HFC-134a.

In one embodiment, any of the disclosed compositions may be generally useful when the tetrafluoropropene is present at about 1 weight percent to about 99 weight percent of the overall composition. In another embodiment, the useful compositions comprise about 20 weight percent to about 99 weight percent tetrafluoropropene. In another embodiment, the useful compositions comprise about 40 weight percent to about 99 weight percent tetrafluoropropene. And in yet another embodiment, the useful compositions comprise about 50 weight percent to about 99 weight percent tetrafluoropropene.

For ternary compositions as described herein, in one embodiment, the compositions may comprise from about 1 weight percent to about 98 weight percent tetrafluoropropene. In another embodiment, the compositions comprise from about 20 weight percent to about 98 weight percent tetrafluoropropene. In another embodiment, the compositions comprise from about 40 weight percent to about 98 weight percent tetrafluoropropene. And in yet another embodiment, the compositions comprise from about 50 weight percent to about 98 weight percent tetrafluoropropene. In certain embodiments, the disclosed compositions comprising trans-HFO-1234ze and HFC-125 contain from about 80 weight percent to about 99 weight percent trans-HFO-1234ze and from about 20 weight percent to about 1 weight percent HFC-125. In other embodiments, the compositions comprise from about 85 weight percent to about 95 weight percent HFO-1234ze and from about 15 weight percent to about 5 weight percent HFC-125.

In some embodiment, the disclosed compositions comprising trans-HFO-1234ze and HFC-32 contain from about 20 weight percent to about 90 weight percent trans-HFO-1234ze and from about 80 weight percent to about 10 weight percent HFC-32.

In one embodiment, the disclosed compositions are generally expected to maintain the desired properties and functionality when the components are present in the concentrations as listed +/−2 weight percent.

In some embodiments, the disclosed compositions are found to be near-azeotropic. Near-azeotropic compositions comprising tetrafluoropropene have been identified at the specified temperature as listed in Table 1.

TABLE 1 Near-azeotrope range Temp Components (weight percent) (° C.) HFO-1234yf/HFC-152a/HFC-134a 1-98/1-98/1-98 23 HFO-1234yf/152a/125 1-98/1-98/1-98 23 HFO-1234yf/HFC-125/HFC-134a 1-98/1-98/1-98 23 HFO-1234yf/HFC-32/HFC-134a 1-98/1-4/1-98 and 23 1-55/45-98/1-55 HFO-1234yf/HFC-134a/ 1-97/1-97/1-97/1-5, 23 HFC-125/HFC-32 1-35/1-40/30-78/6-39, and 1-50/1-40/1-50/40-97

Certain of the compositions of the present invention are non-azeotropic compositions. A non-azeotropic composition may have certain advantages over azeotropic or near azeotropic mixtures. The temperature glide of a non-azeotropic composition provides an advantage in counter current flow heat exchanger arrangements.

In some embodiments, the disclosed compositions are non-flammable as determined using ASTM (American Society of Testing and Materials) E681-2004, the standard test for measuring flammability of refrigerants.

In one embodiment, the composition is a non-flammable composition comprising no more than about 60 weight percent HFO-1234yf and at least about 40 weight percent HFC-134a at about 60° C.

In another embodiment, the composition is a non-flammable composition comprising no more than about 53 weight percent HFO-1234yf and at least about 47 weight percent HFC-134a at about 100° C.

In one embodiment, a refrigerant mixture with some temperature glide may be acceptable in the industry or even have advantages as mentioned previously herein. R407C is an example of a commercial refrigerant product with glide. It has been demonstrated that certain compositions as disclosed herein provide a refrigerant composition with temperature glide that approaches the temperature glide of R407C.

In one embodiment, the compositions comprise at least about 85 weight percent HFO-1234yf and up to about 15 weight percent HFC-32. Such compositions have been demonstrated to have minimal temperature glide and maintain cooling capacity and energy efficiency at a similar level to R407C. In another embodiment, the compositions comprise at least about 90 weight percent HFO-1234yf and up to about 10 weight percent HFC-32. In another embodiment, the compositions comprise at least about 95 weight percent HFO-1234yf and up to about 5 weight percent HFC-32.

In some embodiments, in addition to the tetrafluoropropene and fluorinated compounds, the disclosed compositions may comprise optional other components.

In some embodiments, the optional other components (also referred to herein as additives) in the compositions disclosed herein may comprise one or more components selected from the group consisting of lubricants, dyes, solubilizing agents, compatibilizers, stabilizers, tracers, perfluoropolyethers, anti wear agents, extreme pressure agents, corrosion and oxidation inhibitors, metal surface energy reducers, metal surface deactivators, free radical scavengers, foam control agents, viscosity index improvers, pour point depressants, detergents, viscosity adjusters, and mixtures thereof. Indeed, many of these optional other components fit into one or more of these categories and may have qualities that lend themselves to achieve one or more performance characteristic.

In some embodiments, one or more additive is present in the compositions disclosed in small amounts relative to the overall composition. In some embodiments, the amount of additive(s) concentration in the disclosed compositions is from less than about 0.1 weight percent to as much as about 5 weight percent of total additive. In some the additives are present in the disclosed compositions in an amount between about 0.1 weight percent to about 3.5 weight percent. The additive component(s) selected for the disclosed composition is selected on the basis of the utility and/or individual equipment components or the system requirements.

In some embodiments, the disclosed compositions include at least one lubricant selected from the group consisting of mineral oils (oils of mineral origin), synthetic lubricants, and mixtures thereof.

In some embodiment, the disclosed compositions further comprise at least one lubricant selected from the group consisting of mineral oils, alkylbenzenes, synthetic paraffins, synthetic naphthenes, poly alpha olefins, polyalkylene glycols, dibasic acid esters, polyesters, neopentyl esters, polyvinyl ethers, silicones, silicate esters, fluorinated compounds, phosphate esters and mixtures thereof.

In some embodiments, the disclosed compositions include at least one lubricant selected from those suitable for use with refrigeration or air-conditioning equipment. In some embodiments, the disclosed compositions include at least one synthetic oil selected from those readily known in the field of compression refrigeration lubrication.

In some embodiments, at least one optional component is a mineral oil lubricant. In some embodiments, the mineral oil lubricant is selected from the group consisting of paraffins (including straight carbon chain saturated hydrocarbons, branched carbon chain saturated hydrocarbons, and mixtures thereof), naphthenes (including saturated cyclic and ring structures), aromatics (those with unsaturated hydrocarbons containing one or more ring, wherein one or more ring is characterized by alternating carbon-carbon double bonds) and non-hydrocarbons (those molecules containing atoms such as sulfur, nitrogen, oxygen and mixtures thereof), and mixtures and combinations of thereof.

Some embodiments may contain one or more synthetic lubricant. In some embodiments, the synthetic lubricant is selected from the group consisting of alkyl substituted aromatics (such as benzene or naphthalene substituted with linear, branched, or mixtures of linear and branched alkyl groups, often generically referred to as alkylbenzenes), synthetic paraffins and naphthenes, poly (alpha olefins), polyglycols (including polyalkylene glycols), dibasic acid esters, polyesters, neopentyl esters, polyvinyl ethers (PVEs), silicones, silicate esters, fluorinated compounds, phosphate esters and mixtures and combinations thereof.

In some embodiments, the compositions disclosed herein contain at least one commercially available lubricant. In some embodiments the compositions disclosed herein contain at least one lubricant selected from the group consisting of BVM 100 N (paraffinic mineral oil sold by BVA Oils), Suniso® 1 GS, Suniso® 3GS and Suniso® 5GS (naphthenic mineral oils sold by Crompton Co.), Sontex® 372LT (naphthenic mineral oil sold by Pennzoil), Calumet® RO-30 (naphthenic mineral oil sold by Calumet Lubricants), Zerol® 75, Zerol® 150 and Zerol® 500 (linear alkylbenzenes sold by Shrieve Chemicals) and HAB 22 (branched alkylbenzene sold by Nippon Oil), polyol esters (POEs) such as Castrol® 100 (Castrol, United Kingdom), polyalkylene glycols (PAGs) such as RL-488A from Dow (Dow Chemical, Midland, Mich.), and mixtures thereof.

In other embodiments, at least one of the lubricants further include those lubricants that have been designed for use with hydrofluorocarbon refrigerants and are miscible with compositions as disclosed herein under compression refrigeration and air-conditioning apparatus' operating conditions. In some embodiments, the lubricants are selected by considering a given compressor's requirements and the environment to which the lubricant will be exposed.

In some embodiments, the lubricant is present in an amount of less than 5.0 weight percent to the total composition. In other embodiments, the amount of lubricant is between about 0.1 and 3.5 weight percent of the total composition.

Notwithstanding the above weight ratios for compositions disclosed herein, it is understood that in some heat transfer systems, while the composition is being used, it may acquire additional lubricant from one or more equipment component of such heat transfer system. For example, in some refrigeration, air conditioning and heat pump systems, lubricants may be charged in the compressor and/or the compressor lubricant sump. Such lubricant would be in addition to any lubricant additive present in the refrigerant in such a system. In use, the refrigerant composition when in the compressor may pick up an amount of the equipment lubricant to change the refrigerant-lubricant composition from the starting ratio.

In such heat transfer systems, even when the majority of the lubricant resides within the compressor portion of the system, the entire system may contain a total composition with as much as about 75 weight percent to as little as about 1.0 weight percent of the composition being lubricant. In one embodiment, in some systems, for example supermarket refrigerated display cases, the system may contain about 3 weight percent lubricant (over and above any lubricant present in the refrigerant composition prior to charging the system) and 97 weight percent refrigerant. In another embodiment, in some systems, for example mobile air conditioning systems, the system may contain about 20 weight percent lubricant (over and above any lubricant present in the refrigerant composition prior to charging the system) and about 80 weight percent refrigerant.

In some embodiments, the disclosed compositions include at least one dye. In some embodiments, the disclosed compositions include at least one ultra-violet (UV) dye.

In some embodiments, the disclosed compositions include at least one UV dye that is a fluorescent dye. In some embodiments, the described compositions include at least one UV dye that is a fluorescent dye selected from the group consisting of naphthalimides, perylenes, coumarins, anthracenes, phenanthracenes, xanthenes, thioxanthenes, naphthoxanthenes, fluoresceins, and derivatives of said dye and combinations thereof.

In some embodiments, the disclosed compositions contain from about 0.001 weight percent to about 1.0 weight percent UV dye. In other embodiments, the UV dye is present in an amount of from about 0.005 weight percent to about 0.5 weight percent; and in other embodiments, the UV dye is present in an amount of from 0.01 weight percent to about 0.25 weight percent of the total composition.

In some embodiments, the UV dye is a useful component for detecting leaks of the composition by permitting one to observe the fluorescence of the dye at or in the vicinity of a leak point in an apparatus (e.g., refrigeration unit, air-conditioner or heat pump). One may observe the UV emission, e.g., fluorescence from the dye under an ultra-violet light. Therefore, if a composition containing such a UV dye is leaking from a given point in an apparatus, the fluorescence can be detected at the leak point, or in the vicinity of the leak point.

In some embodiments, the described compositions further contain at least one solubilizing agent selected to improve the solubility of one or more dye in the disclosed compositions. In some embodiments, the weight ratio of dye to solubilizing agent ranges from about 99:1 to about 1:1.

In some embodiments, solubilizing agents in the disclosed compositions include at least one compound selected from the group consisting of hydrocarbons, hydrocarbon ethers, polyoxyalkylene glycol ethers (such as dipropylene glycol dimethyl ether), amides, nitriles, ketones, chlorocarbons (such as methylene chloride, trichloroethylene, chloroform, or mixtures thereof), esters, lactones, aromatic ethers, fluoroethers and 1,1,1-trifluoroalkanes and mixtures thereof.

In some embodiments, at least one compatibilizer is selected to improve the compatibility of one or more lubricant with the disclosed compositions. In some embodiments, the compatibilizer is selected from the group consisting of hydrocarbons, hydrocarbon ethers, polyoxyalkylene glycol ethers (such as dipropylene glycol dimethyl ether), amides, nitriles, ketones, chlorocarbons (such as methylene chloride, trichloroethylene, chloroform, or mixtures thereof), esters, lactones, aromatic ethers, fluoroethers, 1,1,1-trifluoroalkanes, and mixtures thereof.

In some embodiments, one or more solubilizing agent and/or compatibilizer is selected from the group consisting of hydrocarbon ethers consisting of the ethers containing only carbon, hydrogen and oxygen, such as dimethyl ether (DME) and mixtures thereof.

In some embodiments, the disclosed composition includes at least one linear or cyclic aliphatic or aromatic hydrocarbon compatibilizer containing from 5 to 15 carbon atoms. In some embodiments, the compatibilizer is selected from the group consisting of at least one hydrocarbon; in other embodiments, the compatibilizer is a hydrocarbon selected from the group consisting of at least pentane, hexane, octane, nonane, decane, commercially available from Exxon Chemical (USA) under the trademarks Isopar® H (a high purity C₁₁ to C₁₂ iso-paraffinic), Aromatic 150 (a C₉ to C₁₁ aromatic), Aromatic 200 (a C₉ to C₁₅ aromatic) and Naptha 140 and mixtures thereof.

In some embodiments, the disclosed compositions include at least one polymeric compatibilizer. In some embodiments, the disclosed compositions include at least one a polymeric compatibilizer selected from those that are random copolymers of fluorinated and non-fluorinated acrylates, wherein the polymer comprises repeating units of at least one monomer represented by the formulae CH₂═C(R¹)CO₂R², CH₂═C(R³)C₆H₄R⁴, and CH₂═C(R⁵)C₆H₄XR⁶, wherein X is oxygen or sulfur; R¹, R³, and R⁵ areindependently selected from the group consisting of H and C₁-C₄ alkyl radicals; and R², R⁴, and R⁶ are independently selected from the group consisting of carbon-chain-based radicals containing C, and F, and may further contain H, Cl, ether oxygen, or sulfur in the form of thioether, sulfoxide, or sulfone groups and mixtures thereof. Examples of such polymeric compatibilizers include those commercially available from E. I. du Pont de Nemours & Co. (Wilmington, Del., 19898, USA) under the trademark Zonyl® PHS. Zonyl® PHS is a random copolymer made by polymerizing 40 weight percent CH₂═C(CH₃)CO₂CH₂CH₂(CF₂CF₂)_(m)F (also referred to as Zonyl® fluoromethacrylate or ZFM) wherein m is from 1 to 12, primarily 2 to 8, and 60 weight percent lauryl methacrylate (CH₂═C(CH₃)CO₂(CH₂)₁₁CH₃, also referred to as LMA).

In some embodiments, the compatibilizer component contains from about 0.01 to 30 weight percent (based on total amount of compatibilizer) of an additive which reduces the surface energy of metallic copper, aluminum, steel, or other metals and metal alloys thereof found in heat exchangers in a way that reduces the adhesion of lubricants to the metal. Examples of metal surface energy reducing additives include those commercially available from DuPont under the trademarks Zonyl® FSA, Zonyl® FSP, and Zonyl® FSJ.

In some embodiments, the disclosed compositions further include metal surface deactivators. In some embodiments, at least one metal surface deactivator is selected from the group consisting of areoxalyl bis (benzylidene) hydrazide (CAS reg no. 6629-10-3), N,N′-bis(3,5-di-tert-butyl-4-hydroxyhydrocinnamoylhydrazine (CAS reg no. 32687-78-8), 2,2,′-oxamidobis-ethyl-(3,5-di-tert-butyl-4-hydroxyhydrocinnamate (CAS reg no. 70331-94-1), N,N′-(disalicyclidene)-1,2-diaminopropane (CAS reg no. 94-91-7) and ethylenediaminetetra-acetic acid (CAS reg no. 60-00-4) and its salts, and mixtures thereof.

In some embodiments, the compositions disclosed herein further include at least one stabilizer selected from the group consisting of hindered phenols, thiophosphates, butylated triphenylphosphorothionates, organo phosphates, or phosphites, aryl alkyl ethers, terpenes, terpenoids, epoxides, fluorinated epoxides, oxetanes, ascorbic acid, thiols, lactones, thioethers, amines, nitromethane, alkylsilanes, benzophenone derivatives, aryl sulfides, divinyl terephthalic acid, diphenyl terephthalic acid, ionic liquids, and mixtures thereof.

In some embodiments, said at least one stabilizer is selected from the group consisting of tocopherol; hydroquinone; t-butyl hydroquinone; monothiophosphates; and dithiophosphates, commercially available from Ciba Specialty Chemicals, Basel, Switzerland, hereinafter “Ciba”, under the trademark Irgalube® 63; dialkylthiophosphate esters, commercially available from Ciba under the trademarks Irgalube® 353 and Irgalube® 350, respectively; butylated triphenylphosphorothionates, commercially

ilable from Ciba under the trademark Irgalube® 232; amine phosphates, commercially available from Ciba under the trademark Irgalube® 349 (Ciba); hindered phosphites, commercially available from Ciba as Irgafos® 168 and Tris-(di-tert-butylphenyl)phosphite, commercially available from Ciba under the trademark Irgafos® OPH; (Di-n-octyl phosphite); and iso-decyl diphenyl phosphite, commercially available from Ciba under the trademark Irgafos® DDPP; trialkyl phosphates, such as trimethyl phosphate, triethylphosphate, tributyl phosphate, trioctyl phosphate, and tri(2-ethylhexyl)phosphate; triaryl phosphates including triphenyl phosphate, tricresyl phosphate, and trixylenyl phosphate; and mixed alkyl-aryl phosphates including isopropylphenyl phosphate (IPPP), and bis(t-butylphenyl)phenyl phosphate (TBPP); butylated triphenyl phosphates, such as those commercially available under the trademark Syn-O-Ad® including Syn-O-Ad® 8784; tert-butylated triphenyl phosphates such as those commercially available under the trademark Durad®620; isopropylated triphenyl phosphates such as those commercially available under the trademarks Durad® 220 and Durad®110; anisole; 1,4-dimethoxybenzene; 1,4-diethoxybenzene; 1,3,5-trimethoxybenzene; myrcene, alloocimene, limonene (in particular, d-limonene); retinal; pinene; menthol; geraniol; farnesol; phytol; Vitamin A; terpinene; delta-3-carene; terpinolene; phellandrene; fenchene; dipentene; caratenoids, such as lycopene, beta carotene, and xanthophylls, such as zeaxanthin; retinoids, such as hepaxanthin and isotretinoin; bornane; 1,2-propylene oxide; 1,2-butylene oxide; n-butyl glycidyl ether; trifluoromethyloxirane; 1,1-bis(trifluoromethyl)oxirane; 3-ethyl-3-hydroxymethyl-oxetane, such as OXT-101 (Toagosei Co., Ltd); 3-ethyl-3-((phenoxy)methyl)-oxetane, such as OXT-211 (Toagosei Co., Ltd); 3-ethyl-3-((2-ethyl-hexyloxy)methyl)-oxetane, such as OXT-212 (Toagosei Co., Ltd); ascorbic acid; methanethiol (methyl mercaptan); ethanethiol (ethyl mercaptan); Coenzyme A; dimercaptosuccinic acid (DMSA); grapefruit mercaptan ((R)-2-(4-methylcyclohex-3-enyl)propane-2-thiol)); cysteine ((R)-2-amino-3-sulfanyl-propanoic acid); lipoamide (1,2-dithiolane-3-pentanamide); 5,7-bis(1,1-dimethylethyl)-3-[2,3(or 3,4)-dimethylphenyl]-2(3H)-benzofuranone, commercially available from Ciba under the trademark Irganox® HP-136; benzyl phenyl sulfide; diphenyl sulfide; diisopropylamine; dioctadecyl 3,3′-thiodipropionate, commercially available from Ciba under the trademark Irganox® PS 802 (Ciba); didodecyl 3,3′-thiopropionate, commercially available from Ciba under the trademark Irganox® PS 800; di-(2,2,6,6-tetramethyl-4-piperidyl)sebacate, commercially available from Ciba under the trademark Tinuvin® 770; poly-(N-hydroxyethyl-2,2,6,6-tetramethyl-4-hydroxy-piperidyl succinate, commercially available from Ciba under the trademark Tinuvin® 622LD (Ciba); methyl bis tallow amine; bis tallow amine; phenol-alpha-naphthylamine; bis(dimethylamino)methylsilane (DMAMS); tris(trimethylsilyl)silane (TTMSS); vinyltriethoxysilane; vinyltrimethoxysilane; 2,5-difluorobenzophenone; 2′,5′-dihydroxyacetophenone; 2-aminobenzophenone; 2-chlorobenzophenone; benzyl phenyl sulfide; diphenyl sulfide; dibenzyl sulfide; ionic liquids; and mixtures and combinations thereof.

In some embodiments, the disclosed composition includes at least one ionic liquid stabilizer selected from the group consisting of organic salts that are liquid at room temperature (approximately 25° C.), those salts containing cations selected from the group consisting of pyridinium, pyridazinium, pyrimidinium, pyrazinium, imidazolium, pyrazolium, thiazolium, oxazolium and triazolium and mixtures thereof; and anions selected from the group consisting of [BF₄]—, [PF₆]—, [SbF₆]—, [CF₃SO₃]—, [HCF₂CF₂SO₃]—, [CF₃HFCCF₂SO₃]—, [HCCIFCF₂SO₃]—, [(CF₃SO₂)₂N]—, [(CF₃CF₂SO₂)₂N]—, [(CF₃SO₂)₃C]—, [CF₃CO₂]—, and F- and mixtures thereof. In some embodiments, ionic liquid stabilizers are selected from the group consisting of emim BF₄ (1-ethyl-3-methylimidazolium tetrafluoroborate); bmim BF₄ (1-butyl-3-methylimidazolium tetraborate); emim PF₆ (1-ethyl-3-methylimidazolium hexafluorophosphate); and bmim PF₆ (1-butyl-3-methylimidazolium hexafluorophosphate), all of which are available from Fluka (Sigma-Aldrich).

In some embodiments, at least one stabilizer is a hindered phenol, which are any substituted phenol compound including phenols comprising one or more substituted or cyclic, straight chain, or branched aliphatic substituent group, such as, alkylated monophenols including 2,6-di-tert-butyl-4-methylphenol; 2,6-di-tert-butyl-4-ethylphenol; 2,4-dimethyl-6-tertbutylphenol; tocopherol; and the like, hydroquinone and alkylated hydroquinones including t-butyl hydroquinone, other derivatives of hydroquinone; and the like, hydroxylated thiodiphenyl ethers, including 4,4′-thio-bis(2-methyl-6-tert-butylphenol); 4,4′-thiobis(3-methyl-6-tertbutylphenol); 2,2′-thiobis(4methyl-6-tert-butylphenol); and the like, alkylidene-bisphenols including: 4,4′-methylenebis(2,6-di-tert-butylphenol); 4,4′-bis(2,6-di-tert-butylphenol); derivatives of 2,2′- or 4,4-biphenoldiols; 2,2′-methylenebis(4-ethyl-6-tertbutylphenol); 2,2′-methylenebis (4-methyl-6-tertbutylphenol); 4,4-butylidenebis(3-methyl-6-tert-butylphenol); 4,4-isopropylidenebis(2,6-di-tert-butylphenol); 2,2′-methylenebis (4-methyl-6-nonylphenol); 2,2′-isobutylidenebis(4,6-dimethylphenol; 2,2′-methylenebis(4-methyl-6-cyclohexylphenol, 2,2- or 4,4-biphenyldiols including 2,2′-methylenebis(4-ethyl-6-tert-butylphenol); butylated hydroxytoluene (BHT, or 2,6-di-tert-butyl-4-methylphenol), bisphenols comprising heteroatoms including 2,6-di-tert-alpha-dimethylamino-p-cresol, 4,4-thiobis(6-tert-butyl-m-cresol); and the like; acylaminophenols; 2,6-di-tert-butyl-4(N,N′-dimethylaminomethylphenol); sulfides including; bis(3-methyl-4-hydroxy-5-tert-butylbenzyl)sulfide; bis(3,5-di-tert-butyl-4-hydroxybenzyl)sulfide and mixtures and combinations thereof.

In some embodiments, the disclosed compositions contain at least one tracer. In some embodiments, the tracer additive in the disclosed compositions consists of two or more tracer compounds from the same class of compounds or from different classes of compounds.

In some embodiments, the tracer component or tracer blend is present in the compositions at a total concentration of about 50 parts per million by weight (ppm) to about 1000 ppm. In other embodiments, the tracer compound or tracer blend is present at a total concentration of about 50 ppm to about 500 ppm. In other embodiment, the tracer compound or tracer blend is present at a total concentration of about 100 ppm to about 300 ppm.

In some embodiments, the disclosed compositions include at least one tracer selected from the group consisting of hydrofluorocarbons (HFCs), deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodated compounds, alcohols, aldehydes and ketones, nitrous oxide and combinations thereof. Some embodiments of the disclosed compositions include at least one tracer selected from the group consisting of fluoroethane, 1,1,-difluoroethane, 1,1,1-trifluoroethane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,1,3,3-pentafluorobutane, 1,1,1,2,3,4,4,5,5,5-decafluoropentane, 1,1,1,2,2,3,4,5,5,6,6,7,7,7-tridecafluoroheptane, iodotrifluoromethane, deuterated hydrocarbons, deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodated compounds, alcohols, aldehydes, ketones, nitrous oxide (N₂O) and mixtures thereof. In some embodiments, the tracer additive is a tracer blend containing two or more hydrofluorocarbons, or one hydrofluorocarbon in combination with one or more perfluorocarbons.

In some embodiments, at least one tracer composition is added to the disclosed compositions in previously determined quantities to allow detection of any dilution, contamination or other alteration of the composition.

In other embodiments, the compositions disclosed herein may further include a perfluoropolyether. A common characteristic of perfluoropolyethers is the presence of perfluoroalkyl ether moieties. Perfluoropolyether is synonymous to perfluoropolyalkylether. Other synonymous terms frequently used include “PFPE”, “PFAE”, “PFPE oil”, “PFPE fluid”, and “PFPAE”. In some embodiments, the perfluoropolyether has the formula of CF₃—(CF₂)₂—O—[CF(CF₃)—CF₂—O]j′-R′f, and is commercially available from DuPont under the trademark Krytox®. In the immediately preceding formula, j′ is 2-100, inclusive and R′f is CF₂CF₃, a C3 to C6 perfluoroalkyl group, or combinations thereof.

Other PFPEs, commercially available from Ausimont of Milan, Italy, and Montedison S.p.A., of Milan, Italy, under the trademarks Fomblin® and Galden®, respectively, and produced by perfluoroolefin photooxidation, can also be used.

PFPE commercially available under the trademark Fomblin®-Y can have the formula of CF₃O(CF₂CF(CF₃)—O—)_(m′)(CF₂—O—)_(n′)—R_(1f). Also suitable is CF₃O[CF₂CF(CF₃)O]_(m′)(CF₂CF₂O)_(o′)(CF₂O)_(n′)—R_(1f). In the formulae R_(1f) is CF₃, C₂F₅, C₃F₇, or combinations of two or more thereof; (m′+n′) is 8-45, inclusive; and m/n is 20-1000, inclusive; o′ is 1; (m′+n′+o′) is 8-45, inclusive; m′/n′ is 20-1000, inclusive.

PFPE commercially available under the trademark Fomblin®-Z can have the formula of CF₃O(CF₂CF₂—O—)_(p′)(CF₂—O)_(q′)CF₃ where (p′+q′) is 40-180 and p′/q′ is 0.5-2, inclusive.

Another family of PFPE, commercially available under the trademark Demnum™ from Daikin Industries, Japan, can also be used. It can be produced by sequential oligomerization and fluorination of 2,2,3,3-tetrafluorooxetane, yielding the formula of F—[(CF₂)₃—O]_(t′)—R_(2f) where R_(2f) is CF₃, C₂F₅, or combinations thereof and t′ is 2-200, inclusive.

In some embodiments, the PFPE is unfunctionalized. In an unfunctionalized perfluoropolyether, the end group can be branched or straight chain perfluoroalkyl radical end groups. Examples of such perfluoropolyethers can have the formula of C_(r′)F_((2r′+1))-A-C_(r′)F_((2r′+1)) in which each r′ is independently 3 to 6; A can be O—(CF(CF₃)CF₂—O)_(w′), O—(CF₂—O)_(x′)(CF₂CF₂—O)_(y′), O—(C₂F₄—O)_(w′), O—(C₂F₄—O)_(x′)(C₃F₆—O)_(y′), O—(CF(CF₃)CF₂—O)_(x′)(CF₂—O)_(y′), O—(CF₂CF₂CF₂—O)_(w′), O—(CF(CF₃)CF₂—O)_(x′)(CF₂CF₂—O)_(y′)—(CF₂—O)_(z′), or combinations of two or more thereof; preferably A is O—(CF(CF₃)CF₂—O)_(w′), O—(C₂F₄—O)_(w′), O—(C₂F₄—O)_(x′)(C₃F₆—O)_(y′), O—(CF₂CF₂CF₂—O)_(w′), or combinations of two or more thereof; w′ is 4 to 100; x′ and y′ are each independently 1 to 100. Specific examples include, but are not limited to, F(CF(CF₃)—CF₂—O)₉—CF₂CF₃, F(CF(CF₃)—CF₂—O)₉—CF(CF₃)₂, and combinations thereof. In such PFPEs, up to 30% of the halogen atoms can be halogens other than fluorine, such as, for example, chlorine atoms.

In other embodiments, the two end groups of the perfluoropolyether, independently, may be functionalized by the same or different groups. A functionalized PFPE is a PFPE wherein at least one of the two end groups of the perfluoropolyether has at least one of its halogen atoms substituted by a group selected from esters, hydroxyls, amines, amides, cyanos, carboxylic acids, sulfonic acids or combinations thereof.

In some embodiments, representative ester end groups include —COOCH₃, —COOCH₂CH₃, —CF₂COOCH₃, —CF₂COOCH₂CH₃, —CF₂CF₂COOCH₃, —CF₂CF₂COOCH₂CH₃, —CF₂CH₂COOCH₃, —CF₂CF₂CH₂COOCH₃, —CF₂CH₂CH₂COOCH₃, —CF₂CF₂CH₂CH₂COOCH₃.

In some embodiments, representative hydroxyl end groups include —CF₂OH, —CF₂CF₂OH, —CF₂CH₂OH, —CF₂CF₂CH₂OH, —CF₂CH₂CH₂OH, —CF₂CF₂CH₂CH₂OH.

In some embodiments, representative amine end groups include —CF₂NR¹R², —CF₂CF₂NR¹R², —CF₂CH₂NR¹R², —CF₂CF₂CH₂NR¹R², —CF₂CH₂CH₂NR¹R², —CF₂CF₂CH₂CH₂NR¹R², wherein R¹ and R² are independently H, CH₃, or CH₂CH₃.

In some embodiments, representative amide end groups include —CF₂C(O)NR¹R², —CF₂CF₂C(O)NR¹R², —CF₂CH₂C(O)NR¹R², —CF₂CF₂CH₂C(O)NR¹R², —CF₂CH₂CH₂C(O)NR¹R², —CF₂CF₂CH₂CH₂C(O)NR¹R², wherein R¹ and R² are independently H, CH₃, or CH₂CH₃.

In some embodiments, representative cyano end groups include —CF₂CN, —CF₂CF₂CN, —CF₂CH₂CN, —CF₂CF₂CH₂CN, —CF₂CH₂CH₂CN, and —CF₂CF₂CH₂CH₂CN.

In some embodiments, representative carboxylic acid end groups include —CF₂COOH, —CF₂CF₂COOH, —CF₂CH₂COOH, —CF₂CF₂CH₂COOH, —CF₂CH₂CH₂COOH, —CF₂CF₂CH₂CH₂COOH.

In some embodiments, the sulfonic acid end groups is selected from the group consisting of —S(O)(O)OR³, —S(O)(O)R⁴, —CF₂OS(O)(O)OR³, —CF₂CF₂OS(O)(O)OR³, —CF₂CH₂OS(O)(O)OR³, —CF₂CF₂CH₂OS(O)(O)OR³, —CF₂CH₂CH₂OS(O)(O)OR³, —CF₂CF₂CH₂CH₂OS(O)(O)OR³, —CF₂S(O)(O)OR³, —CF₂CF₂S(O)(O)OR³, —CF₂CH₂S(O)(O)OR³, —CF₂CF₂CH₂S(O)(O)OR³, —CF₂CH₂CH₂S(O)(O)OR³, —CF₂CF₂CH₂CH₂S(O)(O)OR³, —CF₂OS(O)(O)OR⁴, —CF₂CF₂OS(O)(O)R⁴, —CF₂CH₂OS(O)(O)R⁴, —CF₂CF₂CH₂OS(O)(O)R⁴, —CF₂CH₂CH₂OS(O)(O)R⁴, —CF₂CF₂CH₂CH₂OS(O)(O)R⁴, wherein R³ is H, CH₃, CH₂CH₃, CH₂CF₃, CF₃, or CF₂CF₃, R⁴ is CH₃, CH₂CH₃, CH₂CF₃, CF₃, or CF₂CF₃.

In some embodiments, the disclosed compositions include additives that are members of the triaryl phosphate family of EP (extreme pressure) lubricity additives, such as butylated triphenyl phosphates (BTPP), or other alkylated triaryl phosphate esters, e.g. Syn-O-Ad® 8478 from Akzo Chemicals, tricresyl phosphates and related compounds. Additionally, the metal dialkyl dithiophosphates (e.g., zinc dialkyl dithiophosphate (or ZDDP), including the commercially available Lubrizol 1375 and other members of this family of chemicals is used in compositions of the disclosed compositions. Other antiwear additives include natural product oils and asymmetrical polyhydroxyl lubrication additives, such as the commercially available Synergol TMS (International Lubricants).

In some embodiments, stabilizers such as antioxidants, free radical scavengers, and water scavengers and mixtures thereof are included. Such additives in this category can include, but are not limited to, butylated hydroxy toluene (BHT), epoxides, and mixtures thereof. Corrosion inhibitors include dodecyl succinic acid (DDSA), amine phosphate (AP), oleoyl sarcosine, imidazone derivatives and substituted sulfphonates.

In one embodiment, the compositions disclosed herein may be prepared by any convenient method to combine the desired amounts of the individual components. A preferred method is to weigh the desired component amounts and thereafter combine the components in an appropriate vessel. Agitation may be used, if desired.

In another embodiment, the compositions disclosed herein may be prepared by a method comprising (i) reclaiming a volume of one or more components of a refrigerant composition from at least one refrigerant container, (ii) removing impurities sufficiently to enable reuse of said one or more of the reclaimed components, (iii) and optionally, combining all or part of said reclaimed volume of components with at least one additional refrigerant composition or component.

A refrigerant container may be any container in which is stored a refrigerant blend composition that has been used in a refrigeration apparatus, air-conditioning apparatus or heat pump apparatus. Said refrigerant container may be the refrigeration apparatus, air-conditioning apparatus or heat pump apparatus in which the refrigerant blend was used. Additionally, the refrigerant container may be a storage container for collecting reclaimed refrigerant blend components, including but not limited to pressurized gas cylinders.

Residual refrigerant means any amount of refrigerant blend or refrigerant blend component that may be moved out of the refrigerant container by any method known for transferring refrigerant blends or refrigerant blend components.

Impurities may be any component that is in the refrigerant blend or refrigerant blend component due to its use in a refrigeration apparatus, air-conditioning apparatus or heat pump apparatus. Such impurities include but are not limited to refrigeration lubricants, being those described earlier herein, particulates including but not limited to metal, metal salt or elastomer particles, that may have come out of the refrigeration apparatus, air-conditioning apparatus or heat pump apparatus, and any other contaminants that may adversely effect the performance of the refrigerant blend composition.

Such impurities may be removed sufficiently to allow reuse of the refrigerant blend or refrigerant blend component without adversely effecting the performance or equipment within which the refrigerant blend or refrigerant blend component will be used.

It may be necessary to provide additional refrigerant blend or refrigerant blend component to the residual refrigerant blend or refrigerant blend component in order to produce a composition that meets the specifications required for a given product. For instance, if a refrigerant blend has three components in a particular weight percentage range, it may be necessary to add one or more of the components in a given amount in order to restore the composition to within the specification limits.

Compositions of the present invention have zero ozone depletion potential and low global warming potential (GWP). Additionally, the compositions of the present invention will have global warming potentials that are less than many hydrofluorocarbon refrigerants currently in use. One aspect of the present invention is to provide a refrigerant with a global warming potential of less than 1000, less than 500, less than 150, less than 100, or less than 50.

Methods of Use

The compositions disclosed herein are useful as heat transfer compositions, aerosol propellants, foaming agents, blowing agents, solvents, cleaning agents, carrier fluids, displacement drying agents, buffing abrasion agents, polymerization media, expansion agents for polyolefins and polyurethane, gaseous dielectrics, fire extinguishing agents, and fire suppression agents. Additionally, in liquid or gaseous form, the disclosed compositions may act as working fluids used to carry heat from a heat source to a heat sink. Such heat transfer compositions may also be useful as refrigerants in a cycle wherein the fluid undergoes phase changes; that is, from a liquid to a gas and back or vice versa.

The compositions disclosed herein may be useful as low GWP (global warming potential) replacements for currently used refrigerants, including but not limited to R134a (or HFC-134a, 1,1,1,2-tetrafluoroethane), R22 (or HCFC-22, chlorodifluoromethane), R404A, (ASHRAE designation for a blend of 44 weight percent R125, 52 weight percent R143a (1,1,1-trifluoroethane), and 4.0 weight percent R134a), R407A, R407B, R407C, R407D, and R407E (ASHRAE designations for blends of R134a, R125 (pentafluoroethane), and R32 (difluoromethane) in differing component concentrations), R408A (ASHRAE designation for a blend of 7 weight percent R125, 46 weight percent R143a, and 47 weight percent R22); R410A (ASHRAE designation for a blend of 50 weight percent R125 and 50 weight percent R32), R413A (ASHRAE designation for a blend containing R218, R134a, and isobutane); R417A, (ASHRAE designation for a blend of 46.6 weight percent R125, 50.0 weight percent R134a, and 3.4 weight percent n-butane), R419A (ASHRAE designation for a blend containing R125, R134a and DME); R422A, R422B, R422C and R422D, (ASHRAE designation for blends of R125, R134a, isobutane in differing component concentrations), R423A (ASHRAE designation for a blend containing R134a and 1,1,1,2,3,3,3-heptafluoropropane (R227ea)); R424A (ASHRAE designation for a blend containing R125, R134a, isobutane, n-butane, and isopentane); R426A (ASHRAE designation for a blend containing R125, R134a, n-butane, and isopentane); R427A (ASHRAE designation for a blend of 15 weight percent R32, 25 weight percent R125, 50 weight percent R134a, and 10 weight percent R143a); R428A (ASHRAE designation for a blend containing R125, R143a, propane and isobutane); R430A (ASHRAE designation for a blend containing R152a and isobutane); R434A (ASHRAE designation for a blend containing R125, R134a, R143a, and isobutane); R437A (ASHRAE designation for a blend containing R125, R134a, n-butane, and n-pentane); R438A (ASHRAE designation for a blend containing R32, R125, R134a, n-butane, and isopentane); R507A and R507B (ASHRAE designation for a blend of R125 and R143a in differing component concentrations); and R508A and R508B (ASHRAE designations for blends of trifluoromethane (R23) and hexafluoroethane (R116) in differing component concentrations).

Additionally, the compositions disclosed herein may be useful as replacements for R12 (CFC-12, dichlorodifluoromethane) or R502 (ASHRAE designation for a blend of 51.2 weight percent CFC-115 (chloropentafluoroethane) and 48.8 weight percent HCFC-22).

Often replacement refrigerants are most useful if capable of being used in the original refrigeration equipment designed for a different refrigerant. In particular, the compositions as disclosed herein may be useful as replacements for R12, R134a, R22, R404A, R407A, R407C, R408A, R410A, R413A, R417A, R419A, R422A, R422B, R422C, R422D, R423A, R424A. R426A, R428A, R430A, R434A, R437A, R438A, R502, R507A, R507B, and R508, among others in original equipment. Additionally, the compositions as disclosed herein may be useful as replacements for R12, R134a, R22, R404A, R407A, R407C, R408A, R410A, R413A, R417A, R419A, R422A, R422B, R422C, R422D, R423A, R424A. R426A, R428A, R430A, R434A, R437A, R438A, R502, R507A, R507B, and R508, among others, in equipment designed for these refrigerants with some system modifications. Further, the compositions as disclosed herein may be useful for replacing any of the above mentioned refrigerants in equipment specifically modified for or produced entirely for these new compositions.

In many applications, some embodiments of the disclosed compositions are useful as refrigerants and provide at least comparable cooling performance (meaning cooling capacity and energy efficiency) as the refrigerant for which a replacement is being sought.

In some embodiments, the compositions disclosed herein are useful for any positive displacement compressor system designed for any number of heat transfer compositions. Additionally, many of the compositions disclosed are useful in new equipment utilizing positive displacement compressors to provide similar performance to the aforementioned refrigerants.

In one embodiment, disclosed herein is a process to produce cooling comprising condensing a composition as disclosed herein and thereafter evaporating said composition in the vicinity of a body to be cooled.

In another embodiment, disclosed herein is a process to produce heat comprising condensing a composition as disclosed herein in the vicinity of a body to be heated and thereafter evaporating said composition.

In some embodiments, the use of the above disclosed compositions includes using the composition as a heat transfer composition in a process for producing cooling, wherein the composition is first cooled and stored under pressure and when exposed to a warmer environment, the composition absorbs some of the ambient heat, expands, and the warmer environment is thusly cooled.

In some embodiments, the compositions as disclosed herein may be useful in particular in air conditioning applications including but not limited to chillers, high temperature heat pumps, residential, commercial or industrial air conditioning systems (including residential heat pumps), and including window, ductless, ducted, packaged terminal, chillers, and those exterior but connected to the building such as rooftop systems.

In some embodiments, the compositions as disclosed herein may be useful in particular in refrigeration applications including high, medium or low temperature refrigeration and other specific uses such as in commercial, industrial or residential refrigerators and freezers, ice machines, self-contained coolers and freezers, supermarket rack and distributed systems, flooded evaporator chillers, direct expansion chillers, walk-in and reach-in coolers and freezers, and combination systems.

Additionally, in some embodiments, the disclosed compositions may function as primary refrigerants in secondary loop systems that provide cooling to remote locations by use of a secondary heat transfer fluid.

In another embodiment is provided a method for recharging a heat transfer system that contains a refrigerant to be replaced and a lubricant, said method comprising removing the refrigerant to be replaced from the heat transfer system while retaining a substantial portion of the lubricant in said system and introducing one of the compositions herein disclosed to the heat transfer system.

In another embodiment, a heat exchange system comprising a composition disclosed herein is provided, wherein said system is selected from the group consisting of air conditioners, freezers, refrigerators, water chillers, flooded evaporator chillers, direct expansion chillers, walk-in coolers, heat pumps, mobile refrigerators, mobile air conditioning units, and systems having combinations thereof.

In another embodiment is provided a method for replacing a high GWP refrigerant in a refrigeration, air-conditioning, or heat pump apparatus, wherein said high GWP refrigerant is selected from the group consisting of R134a, R22, R12, R404A, R410A, R407A, R407C, R413A, R417A, R422A, R422B, R422C and R422D, R423A, R427A, R507A, R507B, R502, and R437A, said method comprising providing a composition as disclosed herein to said refrigeration, air-conditioning, or heat pump apparatus that uses, used or is designed to use said high GWP refrigerant; wherein said composition is selected from the group consisting of:

HFO-1234yf and HFC-32;

HFO-1234yf and HFC-134a;

HFO-1234yf, HFC-152a, and HFC-134a;

HFO-1234yf, HFC-125, and HFC-152a;

HFO-1234yf, HFC-125, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-125;

HFO-1234yf, HFC-32, HFC-125, and HFC-134a;

HFO-1234ze and HFC-32;

HFO-1234ze and HFC-125;

HFO-1234ze, HFC-125, and HFC-152a;

HFO-1234ze, HFC-125, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-125; and

HFO-1234ze, HFC-32, HFC-125, and HFC-134a.

In another embodiment, the method for replacing a high GWP refrigerant may further comprise providing a composition to said refrigeration, air-conditioning, or heat pump apparatus that uses, used or is designed to use said high GWP refrigerant, wherein the composition is selected from the group consisting of:

HFO-1234yf and HFC-32;

HFO-1234yf and HFC-134a;

HFO-1234yf, HFC-152a, and HFC-134a;

HFO-1234yf, HFC-125, and HFC-152a;

HFO-1234yf, HFC-125, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-134a;

HFO-1234yf, HFC-32, and HFC-125;

HFO-1234yf, HFC-32, HFC-125, and HFC-134a;

HFO-1234ze and HFC-32;

HFO-1234ze and HFC-125;

HFO-1234ze, HFC-125, and HFC-152a;

HFO-1234ze, HFC-125, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-134a;

HFO-1234ze, HFC-32, and HFC-125; and

HFO-1234ze, HFC-32, HFC-125, and HFC-134a.

Vapor-compression refrigeration, air-conditioning, or heat pump systems include an evaporator, a compressor, a condenser, and an expansion device. A vapor-compression cycle re-uses refrigerant in multiple steps producing a cooling effect in one step and a heating effect in a different step. The cycle can be described simply as follows. Liquid refrigerant enters an evaporator through an expansion device, and the liquid refrigerant boils in the evaporator, by withdrawing heat from the environment, at a low temperature to form a gas and produce cooling. The low-pressure gas enters a compressor where the gas is compressed to raise its pressure and temperature. The higher-pressure (compressed) gaseous refrigerant then enters the condenser in which the refrigerant condenses and discharges its heat to the environment. The refrigerant returns to the expansion device through which the liquid expands from the higher-pressure level in the condenser to the low-pressure level in the evaporator, thus repeating the cycle.

In one embodiment, there is provided a heat transfer system containing a composition as disclosed herein. In another embodiment is disclosed a refrigeration, air-conditioning, or heat pump apparatus containing a composition as disclosed herein. In another embodiment, is disclosed a stationary refrigeration, air-conditioning, or heat pump apparatus containing a composition as disclosed herein. In yet another embodiment is disclosed a mobile refrigeration or air conditioning apparatus containing a composition as disclosed herein.

In another embodiment, disclosed is a method of using the composition of the present invention as a heat transfer fluid composition. The method comprises transporting said composition from a heat source to a heat sink.

EXAMPLES

The concepts disclosed herein will be further described in the following examples, which do not limit the scope of the invention described in the claims.

Example 1

Impact of Vapor Leakage

A vessel is charged with an initial composition at a temperature of about 23° C., and the initial vapor pressure of the composition is measured. The composition is allowed to leak from the vessel, while the temperature is held constant, until 50 weight percent of the initial composition is removed, at which time the vapor pressure of the composition remaining in the vessel is measured. Results are shown in Table 2.

TABLE 2 After After 50% 50% Delta Composition Initial P Initial P Leak Leak P wt % (Psia) (kPa) (Psia) (kPa) (%) 1234yf/152a/134a 40/40/20 91.0 627 90.5 624  0.5% 20/40/40 88.3 609 87.6 604  0.8% 40/20/40 93.1 642 92.7 639  0.4% 98/1/1 93.5 645 93.5 645  0.0% 1/98/1 81.6 563 81.6 563  0.0% 1/1/98 90.8 626 90.7 625  0.1% 80/10/10 95.0 655 95.0 655  0.0% 10/80/10 84.1 580 83.6 576  0.6% 10/10/80 90.6 625 90.2 622  0.4% 60/20/20 94.3 650 94.2 649  0.1% 20/60/20 86.9 599 86.1 594  0.9% 20/20/60 90.6 625 90.1 621  0.6% 45/45/10 91.2 629 90.7 625  0.5% 10/45/45 86.1 594 85.5 590  0.7% 45/10/45 94.9 654 94.7 653  0.2% 40/30/30 91.9 634 91.4 630  0.5% 30/40/30 89.8 619 89.1 614  0.8% 30/30/40 90.8 626 90.2 622  0.7% 86/4/10 95.1 656 95.0 655  0.1% 86/5/9 95.1 656 95.0 655  0.1% 65/5/30 96.2 663 96.2 663  0.0% 65/30/5 93.6 645 93.4 644  0.2% 5/65/30 84.0 579 83.6 576  0.5% 5/30/65 86.6 597 86.2 594  0.5% 30/5/65 94.5 652 94.2 649  0.3% 30/65/5 88.2 608 87.5 603  0.8% 90/5/5 94.5 652 94.5 652  0.0% 70/5/25 96.1 663 96.1 663  0.0% 1234yf/152a/125 40/40/20 103.4 713 99.0 683  4.3% 20/40/40 114.6 790 106.6 735  7.0% 40/20/40 121.8 840 114.4 789  6.1% 98/1/1 94.2 649 93.8 647  0.4% 1/98/1 82.1 566 81.8 564  0.4% 1/1/98 186.3 1285 185.1 1276  0.6% 80/10/10 101.8 702 99.0 683  2.8% 10/80/10 89.3 616 86.6 597  3.0% 10/10/80 159.8 1102 152.2 1049  4.8% 60/20/20 107.7 743 103.3 712  4.1% 20/60/20 98.4 678 93.6 645  4.9% 20/20/60 136.6 942 127.4 878  6.7% 45/45/10 97.1 669 94.6 652  2.6% 10/45/45 115.5 796 106.5 734  7.8% 45/10/45 129.6 894 121.5 838  6.3% 40/30/30 111.8 771 105.8 729  5.4% 30/40/30 108.9 751 102.7 708  5.7% 30/30/40 118.2 815 110.6 763  6.4% 86/4/10 102.0 703 98.9 682  3.0% 86/5/9 101.1 697 98.4 678  2.7% 65/5/30 118.7 818 111.7 770  5.9% 65/30/5 96.6 666 95.4 658  1.2% 5/65/30 101.2 698 94.3 650  6.8% 5/30/65 134.8 929 124.2 856  7.9% 30/5/65 149.7 1032 141.6 976  5.4% 30/65/5 90.9 627 89.2 615  1.9% 90/5/5 97.9 675 96.3 664  1.6% 70/5/25 114.5 789 108.2 746  5.5% 1234yf/125/134a 40/40/20 130.0 896 122.4 844  5.8% 20/40/40 128.8 888 121.0 834  6.1% 40/20/40 112.9 778 107.9 744  4.4% 98/1/1 94.3 650 93.9 647  0.4% 1/98/1 187.3 1291 186.6 1287  0.4% 1/1/98 91.8 633 91.4 630  0.4% 80/10/10 103.5 714 100.3 692  3.1% 10/80/10 167.5 1155 162.1 1118  3.2% 10/10/80 101.2 698 97.7 674  3.5% 60/20/20 112.9 778 107.7 743  4.6% 20/60/20 147.7 1018 140.0 965  5.2% 20/20/60 111.2 767 105.7 729  4.9% 45/45/10 134.3 926 126.2 870  6.0% 10/45/45 132.3 912 123.7 853  6.5% 45/10/45 104.8 723 102.0 703  2.7% 40/30/30 121.3 836 114.8 792  5.4% 30/40/30 129.6 894 122.1 842  5.8% 30/30/40 120.8 833 114.2 787  5.5% 86/4/10 98.3 678 96.9 668  1.4% 86/5/9 99.1 683 97.3 671  1.8% 65/5/30 100.9 696 99.4 685  1.5% 65/30/5 120.5 831 113.2 780  6.1% 5/65/30 151.1 1042 143.0 986  5.4% 5/30/65 117.8 812 109.9 758  6.7% 30/5/65 99.7 687 98.0 676  1.7% 30/65/5 153.1 1056 145.5 1003  5.0% 90/5/5 98.5 679 96.7 667  1.8% 70/5/25 100.7 694 99.1 683  1.6% 35/35/30 125.4 865 118.4 816  5.6% 50/30/20 121.4 837 114.7 791  5.5% 45/30/25 121.4 837 114.8 792  5.4% 50/25/25 117.2 808 111.3 767  5.0% 45/15/40 108.9 751 104.9 723  3.7% 50/12/38 106.6 735 103.3 712  3.1% 1234yf/32/134a 40/40/20 185.3 1278 167.8 1157  9.4% 20/40/40 176.9 1220 158.6 1094 10.3% 40/20/40 148.4 1023 128.6 887 13.3% 98/1/1 97.8 674 94.7 653  3.2% 1/98/1 231.3 1595 230.9 1592  0.2% 1/1/98 93.5 645 92.1 635  1.5% 80/10/10 130.6 900 111.0 765 15.0% 10/80/10 220.2 1518 215.7 1487  2.0% 10/10/80 117.3 809 105.3 726 10.2% 60/20/20 153.8 1060 131.2 905 14.7% 20/60/20 203.9 1406 193.0 1331  5.3% 20/20/60 142.0 979 123.4 851 13.1% 45/45/10 195.0 1344 180.0 1241  7.7% 10/45/45 179.5 1238 161.6 1114 10.0% 45/10/45 126.0 869 111.5 769 11.5% 40/30/30 168.2 1160 148.0 1020 12.0% 30/40/30 181.2 1249 163.5 1127  9.8% 30/30/40 164.6 1135 144.6 997 12.2% 86/4/10 110.7 763 100.6 694  9.1% 86/5/9 114.3 788 102.0 703 10.8% 65/5/30 114.0 786 104.0 717  8.8% 65/30/5 176.6 1218 152.9 1054 13.4% 5/65/30 202.0 1393 190.1 1311  5.9% 5/30/65 154.1 1062 134.0 924 13.0% 30/5/65 109.8 757 102.0 703  7.1% 30/65/5 214.5 1479 207.8 1433  3.1% 90/5/5 114.1 787 101.4 699 11.1% 70/5/25 110.4 761 103.8 716  6.0% 90/4/6 110.4 761 100.0 689  9.4% 10/40/50 172.3 1188 153.2 1056 11.1% 30/45/25 188.7 1301 172.8 1191  8.4% 20/45/35 184.3 1271 167.5 1155  9.1% 1234yf/134a/125/32 1/1/1/97 231.2 1594 230.9 1592  0.1% 1/1/97/1 188.8 1302 187.8 1295  0.5% 1/97/1/1 94.3 650 92.5 638  1.9% 97/1/1/1 98.6 680 95.2 656  3.4% 50/38/9/3 113.9 785 106.2 732  6.8% 50/38/8/4 116.1 800 107.2 739  7.7% 50/38/7/5 118.4 816 108.2 746  8.6% 20/20/20/40 193.8 1336 180.9 1247  6.7% 10/10/10/70 218.2 1504 213.1 1469  2.3% 5/5/5/85 226.2 1560 224.0 1544  1.0% 5/5/50/40 214.7 1480 210.4 1451  2.0% 50/5/5/40 193.4 1333 176.7 1218  8.6% 10/40/10/40 180.7 1246 163.9 1130  9.3% 37/50/10/3 113.5 783 106.1 732  6.5% 37/10/50/3 148.2 1022 137.8 950  7.0% 50/10/37/3 137.1 945 126.0 869  8.1% 10/50/37/3 132.8 916 122.7 846  7.6% 70/20/8/2 110.2 760 103.5 714  6.1% 20/70/8/2 106.6 735 101.0 696  5.3% 8/20/70/2 162.0 1117 154.3 1064  4.8% 70/8/20/2 119.4 823 110.1 759  7.8% 35/25/30/10 149.2 1029 134.7 929  9.7% 92/1/1/6 118.2 815 102.9 709 12.9% 1/92/1/6 106.3 733 98.5 679  7.3% 1/1/92/6 195.5 1348 193.7 1336  0.9% 74/10/10/6 125.3 864 110.7 763 11.7% 10/74/10/6 116.4 803 106.1 732  8.8% 10/10/74/6 177.0 1220 169.8 1171  4.1% 54/20/20/6 132.6 914 119.0 820 10.3% 20/54/20/6 127.3 878 115.7 798  9.1% 20/20/54/6 158.3 1091 147.7 1018  6.7% 34/30/30/6 138.5 955 126.2 870  8.9% 30/34/30/6 137.9 951 125.7 867  8.8% 30/30/34/6 141.4 975 129.3 891  8.6% 40/27/27/6 136.7 943 124.2 856  9.1% 27/40/27/6 134.7 929 122.8 847  8.8% 27/27/40/6 146.3 1009 134.5 927  8.1% 50/22/22/6 133.6 921 120.5 831  9.8% 22/50/22/6 129.5 893 117.7 812  9.1% 22/22/50/6 154.8 1067 143.7 991  7.2% 88/1/1/10 131.7 908 110.2 760 16.3% 1/88/1/10 115.2 794 103.6 714 10.1% 1/1/88/10 200.1 1380 198.0 1365  1.0% 70/10/10/10 137.5 948 118.6 818 13.7% 10/70/10/10 125.8 867 112.2 774 10.8% 10/10/70/10 182.3 1257 174.5 1203  4.3% 50/20/20/10 143.2 987 127.0 876 11.3% 20/50/20/10 137.1 945 122.9 847 10.4% 20/20/50/10 164.5 1134 152.5 1051  7.3% 40/25/25/10 145.7 1005 130.7 901 10.3% 25/40/40/10 142.7 984 128.4 885 10.0% 25/25/40/10 156.1 1076 142.8 985  8.5% 78/1/1/20 158.6 1094 131.4 906 17.2% 1/78/1/20 135.4 934 117.7 812 13.1% 1/1/78/20 209.3 1443 206.9 1427  1.1% 60/10/10/20 161.9 1116 139.8 964 13.7% 10/60/10/20 146.7 1011 128.7 887 12.3% 10/10/60/20 193.2 1332 184.8 1274  4.3% 40/20/20/20 165.1 1138 147.2 1015 10.8% 20/40/20/20 158.9 1096 141.9 978 10.7% 20/20/40/20 177.0 1220 163.5 1127  7.6% 30/25/25/20 166.5 1148 150.0 1034  9.9% 25/30/25/20 164.9 1137 148.6 1025  9.9% 25/25/30/20 169.4 1168 153.9 1061  9.1% 68/1/1/30 178.4 1230 154.0 1062 13.7% 1/68/1/30 153.1 1056 133.0 917 13.1% 1/1/68/30 215.9 1489 213.8 1474  1.0% 50/10/10/30 179.9 1240 160.6 1107 10.7% 10/50/10/30 164.9 1137 146.2 1008 11.3% 10/10/50/30 201.3 1388 193.3 1333  4.0% 40/15/15/30 180.7 1246 163.4 1127  9.6% 15/40/15/30 171.3 1181 153.8 1060 10.2% 15/15/40/30 193.7 1336 182.2 1256  5.9% 30/20/20/30 181.4 1251 165.6 1142  8.7% 20/30/20/30 177.6 1225 161.5 1114  9.1% 20/20/30/30 186.5 1286 173.0 1193  7.2% 59/1/1/39 191.9 1323 172.8 1191 10.0% 1/59/1/39 167.2 1153 147.4 1016 11.8% 1/1/59/39 220.3 1519 218.6 1507  0.8% 40/10/11/39 192.8 1329 177.80 1226  7.8% 10/40/11/39 180.1 1242 163.20 1125  9.4% 11/10/40/39 206.4 1423 198.70 1370  3.7% 30/15/16/39 193.0 1331 179.30 1236  7.1% 15/30/16/39 186.6 1287 171.70 1184  8.0% 16/15/30/39 199.4 1375 188.90 1302  5.3%

The compositions as listed in Table 2 are near-azeotropic when the composition remaining after 50 weight percent is removed is less than about 10 percent.

Example 2

Glide Reduction

The temperature glide and other cooling performance parameters for a composition containing HFO-1234yf and HFC-32 is determined and displayed in Table 3 as compared to R407C (ASHRAE designation for a refrigerant blend containing 23 wt % HFC-32, 25 wt % HFC 125 and 52 wt % HFC-134a). The glide, pressures, discharge temperatures, COP (energy efficiency) and cooling capacity are determined for the following conditions:

Evaporator temperature  41° F. (5° C.) Condenser temperature 104° F. (40° C.) Subcool amount  41° F. (5° C.) Return gas temperature  59° F. (15° C.) Compressor efficiency is 70%

TABLE 3 Glide, Pres Pres Disch ° C. evap, cond, Temp, Capacity (Cond/ Composition kPa kPa ° C. COP (kJ/m³) Evap) R407C 584 1627 71.3 4.53 3978   5/4.8 HFO-1234yf 371 1016 54.6 4.722 2516 0 HFO-1234yf/HFC-32 (95/5 wt %) 421 1159 57.5 4.598 2799 3.7/2.6 HFO-1234yf/HFC-32 (90/10 wt %) 469 1291 60.1 4.5 3067 5.8/4.4 HFO-1234yf/HFC-32 (85/15 wt %) 515 1412 62.5 4.45 3325 6.9/5.5 HFO-1234yf/HFC-32 (80/20 wt %) 559 1523 64.6 4.416 3575 7.3/6 HFO-1234yf/HFC-32 (78.5/21.5 wt %) 572 1556 65.3 4.408 3648 7.3/6.1 R407C is currently a commercial refrigerant product even with the glide as reported in the table above. This data indicate that HFC-32 concentrations of 15 weight percent or below more closely approach the temperature glide for R407C, which is an amount that has been acceptable in certain applications.

Example 3

Flammability

Flammable compounds may be identified by testing under ASTM (American Society of Testing and Materials) E681-2004, with an electronic ignition source. Such tests of flammability were conducted on compositions of the present disclosure at 101 kPa (14.7 psia), 50 percent relative humidity, and 60° C. or 100° C. at various concentrations in air in order to determine if flammable and if so, find the lower flammability limit (LFL) and the upper flammability limit (UFL). The results are given in Table 4.

TABLE 4 Temperature, ° C. 60° C. 100° C. LFL UFL LFL UFL (vol % in (vol % in (vol % in (vol % in Composition air) air) air) air) HFO-1234yf/HFC-134a non- non- non- non- (50/50 wt %) flammable flammable flammable flammable HFO-1234yf/HFC-134a non- non- non- non- (52.5/47.5 wt %) flammable flammable flammable flammable HFO-1234yf/HFC-134a non- non- 10 10 (53.75/46.25 wt %) flammable flammable HFO-1234yf/HFC-134a non- non- 9.0 10.5 (55/45 wt %) flammable flammable HFO-1234yf/HFC-134a non- non- 8.0 12 (57.5/42.5 wt %) flammable flammable HFO-1234yf/HFC-134a non- non- not tested not tested (60/40 wt %) flammable flammable HFO-1234yf/HFC-134a 10 11 not tested not tested (60.6/39.4 wt %) HFO-1234yf/HFC-134a 8.8 10.8 not tested not tested (62.5/37.5 wt %) HFO-1234yf/HFC-134a 8.0 12 not tested not tested (65/35 wt %)

The results indicate that compositions comprising no more than about 60 weight percent HFO-1234yf and the remainder being HFC-134a are non-flammable at 60° C. Additionally, compositions comprising no more than about 53 weight percent HFC-1234yf and the remainder being HFC-134a are non-flammable at 100° C. Those compositions comprising fluoroolefins that are non-flammable are more acceptable candidates as refrigerant or heat transfer fluid compositions.

Example 4

Global Warming Potentials

Values for global warming potential (GWP) for some of the disclosed compositions are listed in Table 5 as compared to GWP values for HCFC-22, HFC-134a, R404A, R407C, R410A and other currently used refrigerants. The GWP for the pure components are listed for reference. The GWP values for compositions containing more than one component are calculated as weighted averages of the individual component GWP values. The values for the HFCs are taken from the “Climate Change 2007—IPCC (Intergovernmental Panel on Climate Change) Fourth Assessment Report on Climate Change”, from the section entitled “Working Group 1 Report: The Physical Science Basis”, Chapter 2, pp. 212-213, Table 2.14. The value for HFO-1234yf was published in Papadimitriou et al., Physical Chemistry Chemical Physics, 2007, vol. 9, pp. 1-13. Specifically, the 100 year time horizon GWP values are used.

TABLE 5 Component or composition GWP HCFC-22 1810 HFC-134a 1430 HFC-152a 124 HFC-125 3500 HFC-32 675 HFC-143a 4470 HFO-1234ze 6 HFO-1234yf 4 R404A 3922 R407C 1802 R410A 2088 HFO-1234yf/HFC-134a (60/40 wt %) 860 HFO-1234yf/HFC-134a (50/50 wt %) 717 HFO-1234yf/HFC-32 (78.5/21.5 wt %) 148 HFO-1234yf/HFC-32 (85/15 wt %) 105 HFO-1234yf/HFC-32 (90/10 wt %) 71 HFO-1234yf/HFC-32/HFC-125/HFC-134a (35/10/30/25 wt %) 1476 HFO-1234yf/HFC-32/HFC-125/HFC-134a (97/1/1/1 wt %) 57 HFO-1234yf/HFC-32/HFC-125/HFC-134a (1/97/1/1 wt %) 704 HFO-1234yf/HFC-32/HFC-125/HFC-134a (1/1/97/1 wt %) 3415 HFO-1234yf/HFC-32/HFC-125/HFC-134a (1/1/1/97 wt %) 1490 HFO-1234yf/HFC-32/HFC-125/HFC-134a (92/5/1/1 wt %) 87 HFO-1234yf/HFC-32/HFC-125/HFC-134a (50/40/5/5 wt %) 519 HFO-1234yf/HFC-32/HFC-125/HFC-134a (34/6/30/30 wt %) 1520 HFO-1234yf/HFC-32/HFC-125/HFC-134a (1/20/78/1 wt %) 2879 HFO-1234yf/HFC-32/HFC-125/HFC-134a (74/6/10/10 wt %) 254 HFO-1234yf/HFC-32/HFC-125/HFC-134a (27/6/27/40 wt %) 1559 HFO-1234yf/HFC-32/HFC-125 (40/10/50 wt %) 1819 HFO-1234yf/HFC-32/HFC-125 (8/50/42 wt %) 1808 HFO-1234yf/HFC-32/HFC-125 (60/30/10 wt %) 555 HFO-1234yf/HFC-32/HFC-125 (20/20/60 wt %) 2236 HFO-1234yf/HFC-32/HFC-125 (44/20/36 wt %) 1397 HFO-1234yf/HFC-32/HFC-125 (70/15/15 wt %) 629 HFO-1234yf/HFC-32/HFC-125 (70/20/10 wt %) 488 HFO-1234yf/HFC-32/HFC-125 (60/10/30 wt %) 1120 HFO-1234yf/HFC-32/HFC-134a (1/1/98 wt %) 1409 HFO-1234yf/HFC-32/HFC-134a (1/4/95 wt %) 1386 HFO-1234yf/HFC-32/HFC-134a (95/4/1 wt %) 45 HFO-1234yf/HFC-32/HFC-134a (1/98/1 wt %) 676 HFO-1234yf/HFC-32/HFC-134a (98/1/1 wt %) 25 HFO-1234yf/HFC-32/HFC-134a (54/45/1 wt %) 320 HFO-1234yf/HFC-32/HFC-134a (1/45/54 wt %) 1076 HFO-1234yf/HFC-32/HFC-134a (45/45/10 wt %) 320 HFO-1234yf/HFC-32/HFC-134a (30/45/25 wt %) 662 HFO-1234yf/HFC-32/HFC-134a (30/65/5 wt %) 511 HFO-1234yf/HFC-152a/HFC-134a (1/1/98 wt %) 1401 HFO-1234yf/HFC-152a/HFC-134a (1/98/1 wt %) 136 HFO-1234yf/HFC-152a/HFC-134a (98/1/1 wt %) 19 HFO-1234yf/HFC-125/HFC-152a (1/1/98 wt %) 157 HFO-1234yf/HFC-125/HFC-152a (98/1/1 wt %) 40 HFO-1234yf/HFC-125/HFC-152a (1/98/1 wt %) 3431 HFO-1234yf/HFC-125/HFC-134a (1/1/98 wt %) 1436 HFO-1234yf/HFC-125/HFC-134a (1/98/1 wt %) 3444 HFO-1234yf/HFC-125/HFC-134a (98/1/1 wt %) 53 HFO-1234ze/HFC-134a (50/50 wt %) 718 HFO-1234ze/HFC-134a (80/20 wt %) 293 HFO-1234ze/HFC-125 (95/5 wt %) 184 HFO-1234ze/HFC-125 (80/20 wt %) 705 HFO-1234ze/HFC-32 (30/70 wt %) 474 HFO-1234ze/HFC-32 (60/40 wt %) 274 HFO-1234ze/HFC-32 (80/20 wt %) 140

Many compositions as disclosed herein, such as those listed in Table 5, provide lower GWP alternatives to HCFC-22, HFC-134a, R404A, R407C, and/or R410A etc.

Example 5

Cooling Performance

Table 6 shows the performance of some exemplary compositions as compared to HCFC-22, HFC-134a, HFO-1234yf, R410A, and R407C. In Table 6, Evap Pres is evaporator pressure, Cond Pres is condenser pressure, Comp Disch T is compressor discharge temperature, COP is coefficient of performance (analogous to energy efficiency), and CAP is capacity. The data are based on the following conditions.

Evaporator temperature   45° F. (7.2° C.) Condenser temperature  110° F. (43.3° C.) Subcool amount  2.8° F. (5° C.) Return gas temperature   65° F. (18° C.) Compressor efficiency is 70%

Note that the evaporator superheat enthalpy is included in cooling capacity and energy efficiency determinations.

TABLE 6 CAP COP Temp Compr relative relative Glide, Evap Cond Disch to to ° C. Press Press Temp CAP R407C R407C (cond/ Composition (kPa) (kPa) (° C.) (kJ/m³) (%) COP (%) evap) R22 624 1660 85 4112 99.1 4.49 103 0 HFC-134a 377 1110 67 2709 65.3 4.58 105 0 HFO-1234yf 399 1104 59 2564 61.8 4.44 102 0 R410A 991 2589 83 5830 141 4.12 94.7 0.14/0.14 R407C 6.25 1767 76 4151 100 4.36 100  4.8/4.8 HFO-1234yf/HFC-134a 411 1164 62 2763 66.6 4.50 103 0.01 (60/40 wt %) HFO-1234yf/HFC-32 6101 1685 70 3835 92.4 4.29 98.4  7.1/6.1 (78.5/21.5 wt %) HFO-1234yf/HFC-32 578 1603 68 3654 88.0 4.31 98.9   7/5.8 (82/18 wt %) HFO-1234yf/HFC-32 549 1529 67 3493 84.1 4.32 99.3  6.8/5.4 (85/15 wt %)   HFO-1234yf/HFC- 590 1638 67 3738 90.0 4.32 99.1  4.1/3.6 32/HFC-125/HFC-134a   (35/10/30/25 wt %)

Several described compositions have capacity greater than the capacity of HFC-134a, HFO-1234yf and within 10% of the capacity of R407C. Energy efficiency (as displayed as COP), is within 2% of the efficiency for R407C.

Example 6

Heating Performance

Table 7 shows the performance of some exemplary compositions as compared to HCFC-22, HFC-134a, HFO-1234yf, and R410A. In Table 7, Evap Pres is evaporator pressure, Cond Pres is condenser pressure, Comp Disch T is compressor discharge temperature, COP is coefficient of performance (analogous to energy efficiency), and CAP is capacity. The data are based on the following conditions.

Condenser temperature 20° F. (−6.7° C.) Evaporator temperature 80° F. (26.7° C.) Subcool amount 10° F. (5.6° C.) Return gas temperature 65° F. (18° C.) Compressor efficiency is 70%

TABLE 7 CAP COP Temp Compr relative relative Glide, Cond Evap Disch to to ° C. Press Press Temp CAP HCFC- HCFC- (cond/ Composition (kPa) (kPa) (° C.) (kJ/m3) 22 (%) COP 22 (%) evap) R22 397 1091 85 2948 100 4.85 100 0 HFC-134a 228 699 67 1897 64.3 5.02 104 0 HFO-1234yf 249 713 58 1914 64.9 5.03 104 0 R410A 393 1145 75 2965 101 4.74 97.8 0.55/0.52 HFO-1234yf/HFC-134a 251 744 63 2009 68.1 5.03 104  0/0.1 (50/50 wt %) HFO-1234yf/HFC-32 392 1109 69 2812 95.4 4.70 96.9  7.9/6.7 (78.5/21.5 wt %)   HFO-1234yf/HFC- 374 1069 66 2757 93.5 4.80 98.9  4.6/4.1 32/HFC-125/HFC-134a (35/10/30/25 wt %)

Several described compositions have capacity within 7% of the capacity of HCFC-22. Energy efficiency (as displayed as COP) for these compositions is better than or within 4% of the efficiency for HCFC-22.

Example 7

Heating Performance

Table 8 shows the performance of some exemplary compositions as compared to HCFC-22, and HFO-1234yf/HFC-32 compositions. In Table 8, Evap Pres is evaporator pressure, Cond Pres is condenser pressure, Comp Disch T is compressor discharge temperature, COP is coefficient of performance (analogous to energy efficiency), and CAP is capacity. The data are based on the following conditions.

Evaporator temperature   32° C. Condenser temperature −12° C. Subcool amount    9° C. Return gas temperature  −9° C. Compressor efficiency is 70%

TABLE 8 Cond/ Evap 100 yr Compr Avg COP Cap GWP Cond Evap Exit Temp Rel Rel (IPCC Pressure Pressure Temp Glide Capacity to to AR4) (kPa) (kPa) (° C.) (° C.) COP (kJ/m{circumflex over ( )}3) R-22 R-22 HCFC-22 1810 330 1254 76.9 0 4.598 3133.4 100% 103% HFO-1234yf 4 205 824 42.7 0 4.533 1876.1  99%  62% HFO-1234yf/ 105 290 1155 52.3 6.6 4.521 2657.0  98%  88% HFC-32     (85/15 wt %)     HFO-1234yf/ 111 295 1174 52.9 6.7 4.520 2703.7  98%  89% HFC-32     (84/16 wt %)     HFO-1234yf/ 125 305 1211 54.0 6.9 4.517 2795.4  98%  92% HFC-32     (82/18 wt %)     HFO-1234yf/ 138 316 1247 55.1 7.1 4.513 2885.1  98%  95% HFC-32     (80/20 wt %)     HFO-1234yf/ 145 321 1265 55.6 7.1 4.512 2929.1  98%  97% HFC-32 (79/21 wt %)

In heating mode, compositions of HFO-1234yf from 79-85 wt % and HFC-32 from 15-21 wt % have equivalent energy efficiency to R-22 and capacity from 88-97% of R-22. These compositions also have 100 year GWP less than 150 indicating they would be an excellent low GWP replacement for R-22 in heat pumps.

Example 8 Cooling Performance

Table 9 shows the performance of some exemplary compositions as compared to HFC-134a. In Table 9, Evap Pres is evaporator pressure, Cond Pres is condenser pressure, Comp Disch T is compressor discharge temperature, COP is coefficient of performance (analogous to energy efficiency), CAP is cooling capacity, Avg. Temp. glide is the average of the temperature glide in the evaporator and condenser, and GWP is global warming potential. The data are based on the following conditions.

Evaporator temperature   −10° C. Condenser temperature   40.0° C. Subcool amount     6° C. Return gas temperature     10° C. Compressor efficiency is 70%

Note that the evaporator superheat enthalpy is not included in cooling capacity and energy efficiency determinations.

TABLE 9 Compr CAP COP Avg. Evap Cond Disch relative relative Temp. Press Press Temp CAP to 134a to 134a Glide, Composition (kPa) (kPa) (° C.) (kW) (%) COP (%) ° C. GWP* HFC-134a 200.6 1016.5 81.4 2.231 2.742 0 1430 HFO-1234yf 220.5 1015.6 68.3 2.113 94.7 2.580 94.1 0 4 HFO-1234ze/HFC-125 156.7 814.4 76.3 1.769 79 2.756 101 1.61 184 (95/5 wt %) HFO-1234ze/HFC-125 166.6 864.4 76.4 1.869 84 2.746 100 2.96 355 (90/10 wt %) HFO-1234ze/HFC-125 176.9 915.0 76.4 1.968 88 2.735 100 4.08 530 (85/15 wt %) HFO-1234ze/HFC-125 187.7 966.1 76.4 2.067 93 2.718 99 4.99 705 (80/20 wt %) *The GWP value for HFC-134a is taken from the “Climate Change 2007-IPCC (Intergovernmental Panel on Climate Change) Fourth Assessment Report on Climate Change”, from the section entitled “Working Group 1 Report: The Physical Science Basis”, Chapter 2, pp. 212-213, Table 2.14. The value for HFO-1234yf was published in Papadimitriou et al., Physical Chemistry Chemical Physics, 2007, vol. 9, pp. 1-13. Specifically, the 100 year time horizon GWP values are used. The GWP values for the compositions containing HFC-134a and HFO-1234yf are calculated as weighted averages of the individual component GWP values.

The data in Table 9 indicates that the HFO-1234ze/HFC-125 compositions could serve as a replacement for HFC-134a, having performance similar to HFC-134a. In particular, these compositions provide matching energy efficiency (shown as COP), pressures and temperatures in the system, with lower GWP values, and only a minor reduction in cooling capacity. Plus, all the compositions have relatively low temperature glide and a specific composition could be selected based on regulatory requirements for GWP, which have not at this time been determined.

Example 9 Cooling Performance

Table 10 shows the performance of certain compositions as compared to CO₂, R404A (ASHRAE designation for a mixture containing HFC-125, HFC-134a, and HFC-143a), R410A (ASHRAE designation for a mixture containing HFC-32 and HFC-125) and HFC-32. In Table 10, Evap Pres is evaporator pressure, Cond Pres is condenser pressure, Comp Disch T is compressor discharge temperature, COP is coefficient of performance (analogous to energy efficiency), CAP is capacity, Avg. Temp. glide is the average of the temperature glide in the evaporator and condenser, and GWP is global warming potential. The data are based on the following conditions.

Evaporator temperature −35° C. Condenser temperature  −6° C. Subcool amount    0° C. Return gas temperature −25° C. Compressor efficiency is 70%

Note that the evaporator superheat enthalpy is not included in cooling capacity and energy efficiency determinations.

TABLE 10 Compr Avg. Evap Cond Disch Temp. Press Press Temp CAP Glide, Composition (kPa) (kPa) (° C.) (kW) COP ° C. GWP* CO₂ 1204.7 2960.8 57.3 12.132 4.229 0 1 R404A 168.3 449.4 20.0 2.175 4.791 0.5 3922 HFO-1234yf/HFC-32 163.6 503.5 31.5 2.271 4.875 6.7 252 (63/37 wt %) R410A 220.1 654.1 38.3 2.966 4.836 0.1 2088 HFO-1234yf/HFC-32 213.6 635.4 46.4 2.934 4.865 0.8 490 (27.5/72.5 wt %) HFO-1234yf/HFC-32 185.6 561.8 36.9 2.547 4.853 4.3 340 (50/50 wt %) HFO-1234yf/HFC-32 200.2 599.6 41.0 2.739 4.851 2.5 407 (40/60 wt %) HFO-1234yf/HFC-32 218.2 649.8 50.2 3.015 4.852 0.3 541 (20/80 wt %) HFC-32 221.0 666.3 60.8 3.126 4.833 0 675 HFO-1234ze/HFC-32 60.8 220.1 28.6 0.982 4.947 4.7 73 (90/10 wt %) HFO-1234ze/HFC-32 74.7 266.2 33.2 1.201 4.958 7.5 140 (80/20 wt %) HFO-1234ze/HFC-32 89.1 311.4 37.4 1.419 4.968 9.1 207 (70/30 wt %) HFO-1234ze/HFC-32 104.1 356.1 41.4 1.637 4.958 9.8 274 (60/40 wt %) HFO-1234ze/HFC-32 119.6 400.9 45.2 1.855 4.944 9.8 341 (50/50 wt %) HFO-1234ze/HFC-32 135.9 446.6 48.8 2.074 4.927 9.2 407 (40/60 wt %) HFO-1234ze/HFC-32 144.1 469.9 50.6 2.185 4.907 8.6 441 (35/65 wt %) HFO-1234ze/HFC-32 153.0 493.8 52.4 2.298 4.892 8.0 474 (30/70 wt %) HFO-1234ze/HFC-32 162.1 518.4 54.1 2.413 4.875 7.2 508 (25/75 wt %) HFO-1234ze/HFC-32 171.7 543.9 55.7 2.532 4.858 6.2 541 (20/80 wt %) HFO-1234ze/HFC-32 193.1 599.4 58.7 2.793 4.830 3.7 608 (10/90 wt %) *The GWP value for HFCs are taken from the “Climate Change 2007-IPCC (Intergovernmental Panel on Climate Change) Fourth Assessment Report on Climate Change”, from the section entitled “Working Group 1 Report: “The Physical Science Basis”, Chapter 2, pp. 212-213, Table 2.14. The value for HFO-1234yf was published in Papadimitriou et al., Physical Chemistry Chemical Physics, 2007, vol. 9, pp. 1-13. Specifically, the 100 year time horizon GWP values are used. The GWP values for the compositions containing more than one component are calculated as weighted averages of the individual component GWP values.

The composition containing 63 wt % HFO-1234yf and 37 wt % HFC-32 actually shows improved COP and capacity relative to R404A and also has significantly lower GWP. The composition containing 27.5 wt % HFO-1234yf and 72.5 wt % HFC-32 matches the COP and capacity of R410A, has very low temperature glide indicating azeotrope-like behavior and also has significantly lower GWP. Note that all mixtures of tetrafluoropropene (both HFO-1234yf and HFO-1234ze) and HFC-32 have improved COP (energy efficiency) as compared to CO₂, and many have improved COP as compared to R404A and R410A as well. 

What is claimed is:
 1. A composition comprising HFO-1234yf, HFC-32, HFC-125, and HFC-134a; wherein the composition comprises from about 15 weight percent to about 40 weight percent HFO-1234yf, from about 20 weight percent to about 40 weight percent HFC-32, from about 15 weight percent to about 40 weight percent HFC-125, and from about 20 weight percent to about 40 weight percent HFC-134a.
 2. The composition of claim 1 further comprising at least one lubricant selected from the group consisting of mineral oils, alkylbenzenes, synthetic paraffins, synthetic naphthenes, poly alpha olefins, polyalkylene glycols, dibasic acid esters, polyesters, neopentyl esters, polyvinyl ethers, silicones, silicate esters, fluorinated compounds, phosphate esters and mixtures thereof.
 3. A process to produce cooling comprising condensing a composition of claim 1 and thereafter evaporating said composition in the vicinity of a body to be cooled.
 4. A process to produce heat comprising condensing the composition of claim 1 in the vicinity of a body to be heated and thereafter evaporating said composition.
 5. A method for replacing R22, R404A, or R507A in a system that uses, used or was designed to use R22, R404A, or R507A, wherein said method comprises providing the composition of claim 1 to said system.
 6. A refrigeration, air-conditioning or heat pump apparatus containing the composition of claim
 1. 7. A stationary air conditioning apparatus containing the composition of claim
 1. 8. A stationary refrigeration system containing the composition of claim
 1. 9. A stationary heat pump system containing the composition of claim
 1. 